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Prediction of batch heat transfer coefficients for pseudoplastic fluids ...

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.so<br />

respectively..<br />

These contradicting results may be results<br />

<strong>of</strong> complex interactions between the geometrical dimensionless<br />

groups.<br />

As the v.Tidth <strong>of</strong> the impeller blade increases one<br />

would expect the <strong>heat</strong> <strong>transfer</strong> coefficient to increase.<br />

Pratt (149) reports<br />

(2-41<br />

where 1th.<br />

is 1.Jidth <strong>of</strong> the impeller blade and<br />

PH is the diameter <strong>of</strong> the coil helix.<br />

Pursell (150) reports<br />

(2-42<br />

~vhere<br />

Da is the impeller diameter.<br />

Coil Geometry<br />

Oldshue and Gretton (137)r>eport that lrlhen a coil is<br />

used as the <strong>heat</strong> <strong>transfer</strong> surface the coil geometry is<br />

important.<br />

A i

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